Solid-liquid equilibrium measurements of ternary sucrose-mixed solvent mixtures at 25, 40, and 60 °C are carried out, using a simple and accurate analytical method. A search for a reliable activity coefficient model for sugar liquid mixtures is performed: three UNIQUAC based models are investigated - modified UNIQUAC, entropic free-volume and original Flory-Huggins. New UNIQUAC interaction parameters are estimated based on the aqueous and non-aqueous experimental data presented in this work together with those available in the literature. The solubility calculations were carried out using an equation based on fusion enthalpy data for the sugars. Although the UNIQUAC-based models investigated give in general a quite satisfactory representati...
The importance of carbohydrate solutions in many industrial processes is well recognized nowadays. C...
The importance of carbohydrate solutions in many industrial processes is well recognized nowadays. C...
AbstractSolid-liquid equilibria are imperatively required for any design calculations of equipments ...
A simple and accurate apparatus for the measurement of sugar solubilities in mixed solvents using an...
A modified UNIQUAC model with linear temperature-dependent parameters is proposed to describe the th...
New experimental data on the solubilities of D-fructose in the mixed solvents water/ethanol, water/m...
A UNIFAC based model is proposed to describe experimental thermodynamic properties of aqueous and no...
The industrial processing of sugars and sugar-containing mixtures is gaining widespread use as a for...
The industrial processing of sugars and sugar-containing mixtures is gaining widespread use as a for...
In this work, the solubilities of D-glucose in water/methanol and ethanol/methanol mixtures are meas...
PRSV, which is the Peng-Robinson equation of state improved by Stryjek and Vera in 1986, was used to...
In this work the activity of three carbohydrates (sucrose, glucose and fructose) in highly concentra...
In this work the activity of three carbohydrates (sucrose, glucose and fructose) in highly concentra...
In this work the activity of three carbohydrates (sucrose, glucose and fructose) in highly concentra...
The importance of carbohydrate solutions in many industrial processes is well recognized nowadays. C...
The importance of carbohydrate solutions in many industrial processes is well recognized nowadays. C...
The importance of carbohydrate solutions in many industrial processes is well recognized nowadays. C...
AbstractSolid-liquid equilibria are imperatively required for any design calculations of equipments ...
A simple and accurate apparatus for the measurement of sugar solubilities in mixed solvents using an...
A modified UNIQUAC model with linear temperature-dependent parameters is proposed to describe the th...
New experimental data on the solubilities of D-fructose in the mixed solvents water/ethanol, water/m...
A UNIFAC based model is proposed to describe experimental thermodynamic properties of aqueous and no...
The industrial processing of sugars and sugar-containing mixtures is gaining widespread use as a for...
The industrial processing of sugars and sugar-containing mixtures is gaining widespread use as a for...
In this work, the solubilities of D-glucose in water/methanol and ethanol/methanol mixtures are meas...
PRSV, which is the Peng-Robinson equation of state improved by Stryjek and Vera in 1986, was used to...
In this work the activity of three carbohydrates (sucrose, glucose and fructose) in highly concentra...
In this work the activity of three carbohydrates (sucrose, glucose and fructose) in highly concentra...
In this work the activity of three carbohydrates (sucrose, glucose and fructose) in highly concentra...
The importance of carbohydrate solutions in many industrial processes is well recognized nowadays. C...
The importance of carbohydrate solutions in many industrial processes is well recognized nowadays. C...
The importance of carbohydrate solutions in many industrial processes is well recognized nowadays. C...
AbstractSolid-liquid equilibria are imperatively required for any design calculations of equipments ...